Modified collagen

ABSTRACT

The present invention relates to a modified collagen obtainable by providing isolated collagen; freezing the isolated collagen; dehydrating the frozen collagen; and maturing the dehydrated collagen. Also disclosed are methods of preparing the modified collagen and uses thereof.

FIELD OF THE INVENTION

The present invention relates to a modified collagen obtainable byproviding isolated collagen; freezing the isolated collagen; dehydratingthe frozen collagen; and maturing the dehydrated collagen. Alsodisclosed are methods of manufacturing the modified collagen and usesthereof.

BACKGROUND TO THE INVENTION

Processes for the preparation of collagen-based materials for use inhuman and veterinary medicine by drying or lyophilizing aqueous collagendispersions to create membranes or sponges are well known in the art.The use of collagen-based films or membranes as temporary, biodegradablebarriers for separating apposing traumatized tissue surfaces followingsurgery to prevent or reduce the formation of postoperative adhesions isalso known.

Typically, the collagen used for subsequent manufacture of thecollagen-based materials is first isolated by extraction from mammalianhide or tendon, purified, enzymatically-treated to remove thenon-helical telopeptides, partially solubilised with acid, and finallyprecipitated by increasing the pH to provide an aqueous dispersion ofpurified, fibrillar collagen. Once isolated, the collagen dispersion maybe further processed for the manufacture of collagen-based materialsimmediately, or is otherwise stored while waiting further processing.For storage convenience at commercial scale, the collagen dispersion isnormally concentrated by removal of water using centrifugation to reducebulk and thereby create a wet mass. The wet mass must be stored frozento preserve the collagen and prevent bacterial growth. When needed formanufacture of collagen-based materials, the frozen collagen wet mass istypically thawed and redispersed. Whether the isolated collagen is usedimmediately or frozen and thawed as a wet mass, the collagen dispersionis generally viscous and difficult to process at commercial scale intocollagen-based membranes or lyophilized sponges. What is needed is amethod to reduce the viscosity of the collagen dispersion withoutfurther dilution, since reducing the collagen concentration in thedispersion will only increase the amount of water that must be removedon subsequent drying or lyophilizing, which is both inefficient andcostly at commercial scale.

Therefore, the object of the present invention is to modify the isolatedcollagen in such a way as to reduce the viscosity of the dispersion, butwithout compromising the properties of the collagen-based materials madethereof. Preferably, a further object of the present invention is tomodify the collagen in such a way as to reduce the viscosity of thedispersion and also improve the properties of a collagen membrane madethereof for use as a postoperative adhesion barrier.

These objects are solved according to the present invention by providinga modified collagen that facilitates the efficient manufacture ofcollagen-based materials at commercial scale and improves the potentialeffectiveness of those materials in the field of human and veterinarymedicine.

SUMMARY OF THE INVENTION

According to a first aspect of the present invention there is provided amodified collagen obtainable by providing isolated collagen, optionallyan isolated collagen dispersion; freezing the isolated collagen; anddehydrating the frozen collagen.

According to a second aspect of the present invention there is provideda modified collagen obtainable by providing isolated collagen,optionally an isolated collagen dispersion; freezing the isolatedcollagen; dehydrating the frozen collagen; and maturing the dehydratedcollagen.

By the term “dispersion” is meant a mixture in which collagen particlesare dispersed in a fluid, optionally a liquid, further optionally anaqueous, medium. The collagen particles may comprise collagen molecules,or aggregates thereof; which are dispersed in a fluid, optionally aliquid, further optionally an aqueous, medium. Optionally, the collagenparticles, which are dispersed in a fluid, optionally a liquid, furtheroptionally an aqueous, medium; have a length (or maximum dimension) ofat least one micrometer.

By “maturing” is meant processing the dehydrated collagen underconditions suitable to allow ageing of the dehydrated collagen withoutsubstantial degradation or contamination.

According to a third aspect of the present invention there is provided amethod for preparing a modified collagen, the method comprising thesteps of:

-   -   (a) providing isolated collagen, optionally an isolated collagen        dispersion;    -   (b) freezing the isolated collagen; and    -   (c) dehydrating the frozen collagen.

According to a fourth aspect of the present invention there is provideda method for preparing a modified collagen, the method comprising thesteps of:

-   -   (a) providing isolated collagen, optionally an isolated collagen        dispersion;    -   (b) freezing the isolated collagen;    -   (c) dehydrating the frozen collagen; and    -   (d) maturing the dehydrated collagen.

Optionally, the providing step comprises the step of removing the fluid,optionally the liquid, further optionally the aqueous, medium; prior tothe providing step. Further optionally, the providing step comprises thestep of removing at least some of the fluid, optionally the liquid,further optionally the aqueous, medium; prior to the providing step.Still further optionally, the providing step comprises the step ofremoving at least some of the fluid, optionally the liquid, furtheroptionally the aqueous, medium; prior to the providing step; to providean isolated collagen dispersion.

Optionally, the providing step comprises the step of removing the fluid,optionally the liquid, further optionally the aqueous, medium; prior tothe providing step to provide a dispersion having a concentration ofabout 3-30%, optionally 3-4%, (w/w) collagen particles.

Optionally, the freezing step comprises freezing to a temperature ofabout −33° C. to about −42° C. Further optionally, the freezing stepcomprises freezing to a temperature of about −38° C. Still furtheroptionally, the freezing step comprises freezing at a rate of about 0.3°C. to about 1.5° C. per minute, optionally a rate of about 0.5° C. perminute.

Optionally, the dehydrating step comprises removing the aqueous phase.Further optionally, the dehydrating step comprises removing the aqueousphase by reducing the pressure. Still further optionally, thedehydrating step comprises removing the aqueous phase by reducing thepressure to about 0.05 to about 0.5 mbar. Still further optionally, thedehydrating step comprises removing the aqueous phase by applying avacuum.

Optionally or additionally, the dehydrating step comprises increasingthe temperature of the frozen collagen. Further optionally oradditionally, the dehydrating step comprises increasing the temperatureof the frozen collagen under vacuum. Still further optionally oradditionally, the dehydrating step comprises increasing the temperatureof the collagen to about +30° C. Still further optionally oradditionally, the dehydrating step comprises increasing the temperatureof the collagen to about +30° C. under vacuum.

Optionally or additionally, the dehydrating step comprises increasingthe temperature of the collagen to about +30° C. at a rate of about 0.3°C. to about 1.5° C. per minute, further optionally at a rate of about0.5° C. per minute. Further optionally or additionally, the dehydratingstep comprises increasing the temperature of the collagen to about +30°C. at a rate of about 0.3° C. to about 1.5° C. per minute, furtheroptionally at a rate of about 0.5° C. per minute, under vacuum.

Optionally, the dehydrating step comprises at least one equilibratingstep.

Optionally, the at least one equilibrating step comprises maintainingthe temperature at a constant temperature, sufficient to allow thefrozen collagen to reach a desired temperature. Further optionally, theat least one equilibrating step comprises maintaining the temperature ata constant temperature for a sufficient period of time to allow thefrozen collagen to reach a desired temperature. Still furtheroptionally, the at least one equilibrating step comprises maintainingthe temperature at a constant temperature for at least 10 mins,optionally at least 20 mins, further optionally at least 30 mins, stillfurther optionally at least 45 mins, still further optionally at least60 mins; to allow the frozen collagen to reach a desired temperature.

Optionally, the at least one equilibrating step is conducted when thetemperature is increased to at least −20° C. Optionally or additionally,the at least one equilibrating step is conducted when the temperature isincreased to at least −10° C. Optionally or additionally, the at leastone equilibrating step is conducted when the temperature is increased toat least 0° C. Optionally or additionally, the at least oneequilibrating step is conducted when the temperature is increased to atleast +10° C. Optionally or additionally, the at least one equilibratingstep is conducted when the temperature is increased to at least +20° C.Optionally or additionally, the at least one equilibrating step isconducted when the temperature is increased to at least +30° C.

Optionally, the dehydrating step comprises six equilibrating steps, eachequilibrating step being conducted when the temperature is increased byabout 10° C. Further optionally, the dehydrating step comprises sixequilibrating steps, each equilibrating step being conducted when thetemperature is increased to about −20° C., about −10° C., about 0° C.,about +10° C., about +20° C., and about +30° C.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 2° C. Further optionally, the maturing stepcomprises storing the dehydrated collagen at a temperature of at least10° C. Still further optionally, the maturing step comprises storing thedehydrated collagen at a temperature of at least 20° C. Still furtheroptionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 30° C. Still further optionally, thematuring step comprises storing the dehydrated collagen at a temperatureof at least 40° C. Still further optionally, the maturing step comprisesstoring the dehydrated collagen at a temperature of at least 50° C.Still further optionally, the maturing step comprises storing thedehydrated collagen at a temperature of at least 60° C. Still furtheroptionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 70° C. Still further optionally, thematuring step comprises storing the dehydrated collagen at a temperatureof at least 80° C.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 30° C. Further optionally, the maturingstep comprises storing the dehydrated collagen at a temperature of atleast 40° C. Still further optionally, the maturing step comprisesstoring the dehydrated collagen at a temperature of at least 65° C.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of 30° C. Further optionally, the maturing stepcomprises storing the dehydrated collagen at a temperature of 40° C.Still further optionally, the maturing step comprises storing thedehydrated collagen at a temperature of 65° C.

Optionally, the maturing step is conducted for a period of at least oneweek, optionally at least two weeks, further optionally at least threeweeks, still further optionally at least four weeks, still furtheroptionally at least five weeks, still further optionally at least sixweeks.

Optionally, the maturing step is conducted for a period of at least twomonths, optionally at least four months, further optionally at least sixmonths, still further optionally at least twelve months.

Optionally, the maturing step is conducted for a period of one week,optionally two weeks, further optionally three weeks, still furtheroptionally four weeks.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 2° C. for a period of at least six months.Further optionally, the maturing step comprises storing the dehydratedcollagen at a temperature of 2° C. for a period of six months.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 30° C. for a period of at least two months.Further optionally, the maturing step comprises storing the dehydratedcollagen at a temperature of 30° C. for a period of two months.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 40° C. for a period of at least six weeks.Further optionally, the maturing step comprises storing the dehydratedcollagen at a temperature of 40° C. for a period of six weeks.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 65° C. for a period of at least one week.Further optionally, the maturing step comprises storing the dehydratedcollagen at a temperature of 65° C. for a period of one week.

Optionally, the maturing step is conducted at a relative humidity ofless than 100%, optionally less than 90%, further optionally less than80%, still further optionally less than 70%, still further optionallyless than 60%, still further optionally less than 50%, still furtheroptionally less than 40%, still further optionally less than 30%.

By “relative humidity” is meant a measure of the maximum amount of waterin a mixture of gas and water vapour, optionally at a given gastemperature and atmospheric pressure, optionally at constant atmosphericpressure, optionally expressed as a percentage of the maximum amount ofwater vapour within the gas at the given gas temperature and atmosphericpressure. For the purposes of this specification, the term “relativehumidity” is intended to mean a measure of the amount of water vapour ina mixture of environmental air and water vapour, in which the maturingstep is conducted, at a constant atmospheric pressure, and expressed asa percentage. For the purposes of this specification, atmosphericpressure understood to be about 980 to about 1040 millibars.

It is understood that, in conducting the maturing step, the parametersof temperature, time, pressure, and relative humidity are notnecessarily mutually exclusive, and the skilled person would recognisethat as one parameter is varied, one or both of the other parameters mayalso be varied accordingly.

Optionally, the maturing step comprises storing the dehydrated collagenat a temperature of at least 40° C. for a period of at least six weeks,and at a relative humidity of less than 80%. Further optionally, thematuring step comprises storing the dehydrated collagen at a temperatureof 40° C. for a period of 6 weeks, and at a relative humidity of 75%.

Optionally, the isolated collagen is fibrillar collagen. Furtheroptionally, the isolated collagen is selected from Type I collagen, TypeII collagen, Type Ill collagen, and a mixture thereof. Still furtheroptionally, the isolated collagen is Type I collagen.

Optionally, the method further comprises the step of mechanicallydegrading the modified collagen prior to the maturing step. Optionally,the mechanical degrading step comprises milling. Further optionally, themechanical degrading step is selected from milling, cutting, grinding,and a mixture thereof.

According to a fifth aspect of the present invention there is provided amethod for isolating collagen, the method comprising the steps of:

-   -   (a) providing a collagen source; and    -   (b) increasing the pH of the collagen source to about 6.5 to        about 7.5.

Optionally, the collagen source is a collagen dispersion.

Optionally, the providing step comprises the step of removing the fluid,optionally the liquid, further optionally the aqueous, medium; prior tothe providing step. Further optionally, the providing step comprises thestep of removing at least some of the fluid, optionally the liquid,further optionally the aqueous, medium; prior to the providing step.Still further optionally, the providing step comprises the step ofremoving at least some of the fluid, optionally the liquid, furtheroptionally the aqueous, medium; prior to the providing step; to providean isolated collagen dispersion.

Optionally, the pH of the collagen source, optionally the collagendispersion, is increased to about 7.5.

Optionally, the collagen source is a fibrous tissue, optionallyconnective tissue. Further optionally, the collagen source is tendon,optionally animal tendon, further optionally equine or bovine tendon,preferably equine tendon.

Optionally, the method comprises the step of degrading the collagensource prior to the pH-increasing step. Further optionally, thedegrading step comprises mechanically degrading the collagen sourceprior to the pH-increasing step. Optionally or additionally, thedegrading step comprises chemically degrading the collagen source priorto the pH-increasing step.

Optionally, the mechanical degrading step comprises milling. Furtheroptionally, the mechanical degrading step is selected from milling,cutting, grinding, granulating, and a mixture thereof. Optionally oradditionally, the chemical degrading step comprises contacting thecollagen source with an enzyme, optionally a proteolytic enzyme.Optionally, the proteolytic enzyme is selected from chymosin, cathepsinE, and pepsin; preferably pepsin.

Optionally, the chemical degrading step is conducted at a pH of about2.5.

Optionally, the method further comprises the step of removingcontamination from the collagen source. Optionally, the removing stepcomprises contacting the collagen source with a base, optionally astrong base, further optionally sodium hydroxide, still furtheroptionally an aqueous solution of sodium hydroxide.

Optionally, the method comprises the step of filtering the degradedcollagen source, optionally the degraded collagen dispersion, prior tothe pH-increasing step.

Optionally, the method comprises the step of concentrating the collagen.Optionally, the concentrating step comprises isolating the collagen.Further optionally, the concentrating step comprises isolating thecollagen by centrifugation.

Optionally, the concentrating step comprises the step of removing thefluid, optionally the liquid, further optionally the aqueous, medium; toprovide a dispersion having a concentration of about 3-30%, optionally3-4%, (w/w) collagen particles.

Optionally, the isolated collagen is frozen. Further optionally, theisolated collagen is frozen at less than −20° C. Optionally, the frozenisolated collagen is thawed prior to preparing the modified collagen.

According to a sixth aspect of the present invention, there is provideda composition comprising a modified collagen according to a first aspectof the present invention, or a modified collagen prepared according to asecond aspect of the present invention, for use in treating orpreventing surgical adhesions.

Optionally, use comprises the administration of the composition at abiological membrane, optionally a biological tissue. Further optionally,use comprises the administration of the composition at a biologicalmembrane, optionally a biological tissue, within a body cavity. Stillfurther optionally, use comprises the administration of the compositionat a biological membrane, optionally a biological tissue, within a bodycavity such as a peritoneal cavity, a pericardial cavity, a uterinecavity, or a synovial cavity.

Optionally, use comprises the topical administration of the compositionat a biological membrane, optionally a biological tissue. Furtheroptionally, use comprises the topical administration of the compositionat a biological membrane, optionally a biological tissue, within a bodycavity. Still further optionally, use comprises the topicaladministration of the composition at a biological membrane, optionally abiological tissue, within a body cavity such as a peritoneal cavity, apericardial cavity, a uterine cavity, or a synovial cavity.

According to a seventh aspect of the present invention there is provideda method for the manufacture of a composition comprising a modifiedcollagen according to a first aspect of the present invention or amodified collagen prepared according to a second aspect of the presentinvention, the method comprising the steps of:

-   -   (a) providing a modified collagen;    -   (b) preparing an aqueous dispersion of the modified collagen;    -   (c) degrading the aqueous dispersion; and    -   (d) dehydrating the aqueous dispersion.

Optionally, the preparing step comprises adding heated water, optionallyheated purified water, to the modified collagen. Optionally, the water,optionally the purified water is heated to about 35 to about 42° C.prior to adding to the modified collagen.

Optionally, the preparing step is conducted at a pH of about 4.0.

Optionally, the degrading step comprises mechanically degrading theaqueous dispersion.

Optionally, the mechanical degrading step comprises shear mixing.

Optionally, the composition comprises modified collagen in an amount ofabout 0.4% to 1.5% (w/w).

Optionally, the composition has a pH of about 4.0.

Optionally, the dehydrating step comprises removing liquid from theaqueous dispersion such that the composition comprises liquid in anamount of less than 30%, optionally less than 20%, further optionallyless than 15% (w/w) of the composition. Further optionally, thedehydrating step comprises removing liquid from the aqueous dispersionsuch that the composition comprises liquid in an amount of less than13%, preferably less than 12%, (w/w) of the composition.

Optionally, the dehydrating step comprises removing liquid from theaqueous dispersion using a convective drying cabinet.

According to an eighth aspect of the present invention there is provideda drug delivery composition obtainable by providing isolated collagen,optionally an isolated collagen dispersion; freezing the isolatedcollagen; and dehydrating the frozen collagen.

According to a ninth aspect of the present invention there is provided adrug delivery composition obtainable by providing isolated collagen,optionally an isolated collagen dispersion; freezing the isolatedcollagen; dehydrating the frozen collagen; and maturing the dehydratedcollagen.

According to a tenth aspect of the present invention, there is provideda method of preparing a drug delivery composition for sustained drugrelease, the method comprising the steps of:

-   -   (a) providing isolated collagen, optionally an isolated collagen        dispersion;    -   (b) freezing the isolated collagen; and    -   (c) dehydrating the frozen collagen.

According to an eleventh aspect of the present invention, there isprovided a method of preparing a drug delivery composition for sustaineddrug release, the method comprising the steps of:

-   -   (a) providing isolated collagen, optionally an isolated collagen        dispersion;    -   (b) freezing the isolated collagen;    -   (c) dehydrating the frozen collagen; and    -   (d) maturing the dehydrated collagen.

Optionally, the method further comprises the step of providing a drug,optionally a drug solution, to which the matured collagen is added, orwhich is added to the matured collagen.

Optionally, the drug is selected from an aminoglycoside antibiotic, or asalt or prodrug thereof; and an anaesthetic, or a salt or prodrugthereof.

Further optionally, the drug is selected from gentamicin((3R,4R,5R)-2-{[(1S,2S,3R,4S,6R)-4,6-diamino-3-{[(2R,3R,6S)-3-amino-6-[(1R)-1-(methylamino)ethyl]oxan-2-yl]oxy}-2-hydroxycyclohexyl]oxy}-5-methyl-4-(methylamino)oxane-3,5-diol),or a salt or prodrug thereof; and bupivacaine((RS)-1-butyl-N-(2,6-dimethylphenyl)piperidine-2-carboxamide), or a saltor prodrug thereof.

Optionally, the drug is an aqueous drug solution. Further optionally,the drug is an aqueous drug solution comprising an acid, optionallyacetic acid.

Optionally, the method further comprises the step of mixing, optionallyhomogenizing, the drug-, optionally drug solution-, containing drugdelivery composition.

Optionally, the method further comprises the step of lyophilizing and/ordehydrating, the drug-, optionally drug solution-, containing drugdelivery composition.

BRIEF DESCRIPTION OF THE DRAWINGS

Embodiments of the present invention will now be described withreference to the following non-limiting examples and the accompanyingdrawings wherein the error bars represent standard deviations, in which:

FIG. 1 is a graph illustrating the viscosity characteristic ofcompositions prepared from fresh collagen, frozen collagen, anddehydrated frozen collagen, which was allowed to age under ambientconditions for 3 years (old lyophilised milled collagen);

FIG. 2A is a graph illustrating the water uptake characteristic ofcompositions prepared from fresh collagen, frozen collagen, anddehydrated frozen collagen, which was allowed to age under ambientconditions for 3 years (old lyophilised milled collagen);

FIG. 2B is a graph illustrating the swelling characteristic ofcompositions comprising fresh collagen, frozen collagen, and dehydratedfrozen collagen, which was allowed to age under ambient conditions for 3years (old lyophilised milled collagen);

FIG. 3A is a graph illustrating the dissolution characteristic ofgentamicin-containing compositions prepared from frozen collagen anddehydrated frozen collagen, which was allowed to age under ambientconditions for 3 years (old lyophilised milled collagen);

FIG. 3B is a graph illustrating the dissolution characteristic ofbupivacaine-containing compositions prepared from frozen collagen anddehydrated frozen collagen, which was allowed to age under ambientconditions for 3 years (old lyophilised milled collagen);

FIG. 4 is a graph illustrating the viscosity characteristic ofcompositions prepared from fresh collagen, frozen collagen, dehydratedfrozen collagen, which was allowed to age under ambient conditions for 3years (old lyophilised milled collagen), dehydrated frozen collagen(non-matured LMC), and a modified collagen according to a first aspectof the present invention, matured for 2, 4, and 6 weeks (LMC matured);

FIG. 5 is a graph illustrating the viscosity characteristic ofcompositions prepared from dehydrated frozen collagen (non-maturedlyophilised milled collagen), and a modified collagen according to afirst aspect of the present invention (LMC matured);

FIG. 6 is a graph illustrating the relative swelling ability ofcompositions prepared from frozen collagen (FWC) and dehydrated frozencollagen, which was allowed to age under ambient conditions for 3 years(old LMC); frozen collagen (FWC) and a modified collagen according to afirst aspect of the present invention (LMC matured); and dehydratedfrozen collagen (non-matured LMC) and a modified collagen according to afirst aspect of the present invention (LMC matured);

FIG. 7 is a graph illustrating the degradation characteristic ofcompositions prepared from dehydrated frozen collagen (non-matured LMC),and a modified collagen according to a first aspect of the presentinvention (LMC matured);

FIG. 8A is a graph illustrating the dissolution characteristic ofgentamicin-containing compositions prepared from frozen collagen (FWC),dehydrated frozen collagen (non-matured LMC), and a modified collagenaccording to a first aspect of the present invention (LMC matured);

FIG. 8B is a graph illustrating the dissolution characteristic ofbupivacaine-containing compositions prepared from dehydrated frozencollagen, which was allowed to age under ambient conditions for 3 years(old LMC), and dehydrated frozen collagen (non-matured LMC); and

FIG. 9 is a graph illustrating the illustrating the viscositycharacteristic of a modified collagen according to a first aspect of thepresent invention, matured for up to 4 weeks (LMC matured).

EXAMPLES Example 1 Collagen Isolation

Collagen can be isolated from a number of sources, for example, animalhides and animal tendons. In a preferred embodiment, the collagen isisolated from animal tendon, for example equine or bovine tendon;although any known source of collagen, including fibrous tissue,optionally connective tissue, may be used and selected by one skilled inthe art. Preferably, the collagen is isolated from equine tendon. In themethod of isolation, equine tendons were milled to degrade the collagensource. The milled equine tendons were treated with a number ofreagents, including 1N sodium hydroxide (NaOH) to remove microbiologicalcontamination such as prions at the beginning of the process. Treatmentsteps with hydrogen peroxide and washing steps at different pH valueswere conducted, followed by a milling step, which was used to increasethe surface for the next treatment step. The molecular weight of thecollagen source was additionally reduced by treatment with theproteolytic enzyme pepsin at an approximate pH of 2.5. The pH wasadjusted using an aqueous solution of 1N HCl. The pepsin was used todegrade contaminating serum components such as equine serum albumin(ESA) and resulted in the detachment of non-helical portions of thecollagen molecule (telopeptides). During this process, the collagenmaterial was also partially solubilised in the acidic medium. Afterfiltration, the pH level was increased from 2.5 to 7.5 by addition of 1Nsodium hydroxide (NaOH). This pH adjustment resulted in precipitation ofthe fibrillar collagen out of solution, which was then concentrated bymeans of centrifugation to provide a collagen dispersion having aconcentration of about 3-30% (w/w). The resulting material wasdesignated fresh collagen. The fresh collagen can be processed inseveral ways.

The fresh collagen can be packaged in suitable portions and frozen to−20° C. to be stored in a freezer until required for use. The resultingmaterial was designated frozen collagen (FWC). The frozen collagen isthawed prior to use in the same manner as fresh collagen.

Alternatively, frozen collagen can be freeze-dried (lyophilised), andoptionally subsequently milled. For this purpose, frozen collagen wasmanually distributed onto a flat surface, for example a polystyrenemould, the frozen collagen having a layer thickness of between about 5mm and about 10 mm. The collagen-filled moulds were transferred onto theshelves of a commercially available freeze dryer (Christ Epsilon) andfrozen to a temperature of about −38° C. with a ramp rate between 0.3°C. and 1.5° C. After an equilibration period of approximately 30 minutesvacuum was initiated and the shelf temperature was sequentiallyincreased from about −38° C. to about +30° C. at a rate of about 0.5° C.per minute. The combination of vacuum and sequentially increasing theshelf temperature from about −38° C. to about +30° C. facilitatedsublimation of the ice from the frozen collagen up until the collagenreached a temperature of 0° C. To ensure that the temperature of thecollagen increased uniformly, at least one equilibrating step wasconducted, in which the shelf temperature was maintained at a constantdesired temperature for approximately 30 mins, or until the collagenreached the desired temperature. For example, an equilibrating step wasconducted every 10° C. between the temperatures of −20° C. and +30° C.to ensure that the temperature of the collagen increased uniformly. Theequilibrating step, for example at −20° C. comprised maintaining theshelf temperature at a constant temperature of −20° C. for about 30mins. Once the ice had been removed by sublimation, and the collagenreached a temperature of 0° C., the residual water content was furtherreduced by continuing to sequentially increase the shelf temperature toabout +30° C. at a rate of about 0.5° C. per minute. The lyophilisedcollagen was then milled using a commercially available cutting mill(Rotoplex, Hosokawa Alpine). The resulting material was designatednon-matured lyophilised milled collagen (non-matured LMC).

Optionally, the non-matured lyophilised milled collagen was matured bystoring in polyethylene containers (bags) under ambient conditions ofabout 2-8° C. at atmospheric pressure for periods of about 1-3 yearsuntil required for use. The resulting material was designated oldlyophilized milled collagen (old LMC).

Alternatively, the non-matured lyophilized milled collagen (non-maturedLMC) was matured by storing in polyethylene containers (bags) asdescribed herein until required for use, for example stored at 40° C.for 2-6 weeks. The resulting material was designated matured lyophilizedmilled collagen (matured LMC).

Example 2 Compounding Process and Equipment

An aqueous modified collagen dispersion was prepared in a stainlesssteel vessel using pre-heated (35-42° C.) purified water, which wasadjusted to pH 4.0±0.2. High shear mixing was required to break up themodified collagen mass and expose the collagen fibres to the acidicmedium. The high shear mixer (homogeniser) comprised a rotor/stator headthat is designed to create high shear forces by pulling the modifiedcollagen through the rotating homogeniser head and forcing the modifiedcollagen against the proximal stationary stator head. It is this designthat provided the high shear forces required to separate the fibrouscollagen mass at the beginning of the aqueous dispersion preparation.However, other comparable mixing equipment may also be used; and can beselected by one skilled in the art. For example, an IKA Ultra-Turraxmixer may be used at a high speed for about 2 to about 5 minutes.

If required, although not essential, the resulting aqueous dispersioncan be filtered and degassed, for example by using 250 micron filtersand a suitable means of degassing, for example ultrasonication.

The collagen concentration in the final aqueous dispersion can be in therange of 0.4% to 1.5% and the pH can be in the range of 4.0±0.2. Thefinal aqueous dispersion can be subsequently transferred to a closedjacketed stainless steel vessel, optionally where the jacket temperatureis maintained at 37° C. and the aqueous dispersion is slowly agitatedusing a low shear setting.

The dispersion was filled into, for example 10×10 cm, blister trays orlyophilisation moulds using, for example, a positive displacement pump.The pump can be a valve-less pump, optionally having ceramic pistons.Alternatively, a peristaltic pump could also be used. The fill weightwas adjusted based on the collagen content of the aqueous dispersion toachieve the target collagen content per area, for example about 0.1 toabout 10.0 mg/cm², optionally about 4 mg/cm². Upon completion of thefilling process, the filled blisters or moulds were placed into aconvective drying cabinet. A commercially available drying cabinet(LabAir; Bleymehl) at 31° C. was utilized for this drying process. Thedrying step can typically require between 1 and 3 days to remove theexcess water, which results in the finished composition, for examplemembrane, being retained in the blisters or moulds.

Following completion of the drying process, the blisters or moulds wereremoved from the drying cabinet. The resulting composition, for examplemembrane, was cut to the desired size, for example using a pneumaticdye. The packaging process was a two-step process comprisingintroduction to an inner and outer pouch packaging (ethylene oxide; EOtype; PMS MEDICAL LTD) followed by pneumatic heat sealing. One side ofthe outer pouch comprised a transparent polyester or low-densitypolyethylene (LDPE) foil laminate with a high-density polyethylene(HDPE) strip seal. The other side was an opaque polyester or LDPElaminate. Other outer pouch packaging material can be used, includingaluminum oxide coated polyethylene materials or, if E-beam radiation isused for sterilization, an aluminum outer pouch can be used. Thepneumatic heat sealer facilitated the formation of a continuous seal atthe open end of the pouch. The top part of the pouch included two holesor strips lined with a high-density polyethylene (HDPE) strip seal.These openings/windows were specifically designed for the EO gassterilisation process and were gas permeable only. The permeability ofthe window facilitated permeation of the EO gas during the terminal EOsterilization process. Following sterilization and ventilation, theouter pouch was resealed below the gas permeable openings/windows, andthis gas permeable (top) portion was then removed from the pouch. Thisresulted in a fully sealed outer pouch containing a terminallysterilized finished composition, for example membrane.

Ethylene Oxide (EO; C₂H₄O) is a gas that, at appropriate operatingtemperatures, sterilises via the action as a powerful alkylating agent.Under the correct conditions, cellular constituents of organisms such asnucleic acid complexes, functional proteins, and enzymes will react withethylene oxide, causing the addition of alkyl groups. As a result of thealkylation, cell reproduction is prevented and cell death ensues. Thesterilizer used in the present Examples was a DMB 15009 VD (DMBApparatebau GmbH, Germany). A mixture of EO/CO₂ at a ratio of 15:85 wasused as the sterilization gas over a period of 6 hours at 4 barpressure. For successful completion of this process, the product needsto contain a moisture level of not less than 9%, which can be achievedby holding it in an area under controlled environmental conditions.Following the EO sterilization process, the product was ventilated for aminimum of 3 to 4 weeks to reduce the level of remaining ethylene oxidegas and any residues from the composition, for example membrane, andpackaging materials.

Example 3 Characterisation

All compositions (membranes) were prepared from a 0.6% dispersion usingthe method described herein above. All tests on the collagen dispersionwere conducted within 1 day after compounding; and all characterisationexperiments with the membranes were performed within 1 month aftermembrane manufacture using unsterilised membranes.

Dispersion Viscosity

The viscosity values of 0.9% collagen dispersions prepared from each ofthe fresh collagen, frozen collagen, non-matured lyophilised milledcollagen, and matured lyophilised milled collagen according 15 toExample 2 were measured using a Brookfield viscometer (Digital RheometerDV-III+ with associated TC-501 Circulating Bath). The viscosity valueswere measured at a constant shear rate (15 s⁻¹) and over a temperaturerange from 25 to 40° C. at 5° C. increments. 60 measurements pertemperature were averaged to obtain reliable results.

The dispersion viscosity depends on the temperature and decreases whenheating up the dispersion. The viscosity profiles of fresh and frozencollagen are comparable over the temperature range tested. Thelyophilised milled collagen, which was stored at a temperature of 2-8°C. for 3 years before compounding (old LMC), showed significantly lowerviscosity at all investigated temperatures compared to the freshcollagen and the frozen collagen (see FIG. 1). Lyophilised milledcollagen, which was compounded without storage (non-matured LMC), showedlower viscosity at all investigated temperatures compared to the freshcollagen and the frozen collagen (see FIG. 4). Lyophilised milledcollagen, which was matured (stored at a temperature of 40° C. beforecompounding; matured LMC), showed lower viscosity compared tonon-matured LMC (see FIG. 4), and comparable with old lyophilised milledcollagen.

As can be seen in FIG. 5, maturing the lyophilised milled collagen asdescribed herein results in improved viscosity at all investigatedtemperatures compared to non-matured lyophilised milled collagen, whichis not subjected to the maturing step described herein.

The difference in viscosity is an advantage for processing of themembranes. Collagen with lower viscosity can be more easily degassed,and filled or casted; and the drying time is also reduced as collagenshaving higher concentrations can be processed. The modified collagen ofthe present invention provides improved viscosity characteristicscompared to fresh collagen and frozen collagen; and the maturing stepprovides comparable viscosity characteristics compared to lyophilisedmilled collagen, which was stored at a temperature of 2-8° C. for 3years before compounding (old LMC), thereby providing the improvedviscosity characteristics of aged collagen (old LMC) without theextended ageing period.

Water Uptake and Swelling

Three rectangular samples (1.5×4 cm in size) were cut from 5 membranesprepared from each of the fresh collagen, frozen collagen, oldlyophilised milled collagen, and matured lyophilised milled collagen.Each of these samples was soaked in WFI (water for injection) for 10minutes, and analysed regarding water uptake (wet weight—dry weight) andswelling (wet thickness—dry thickness). The sample thickness wasmeasured using a Mitutoyo Micrometer IP54.

Membranes prepared from lyophilised milled collagen, which was stored ata temperature of 2-8° C. for 3 years before compounding (old LMC),showed lower water uptake and swelling than membranes prepared fromfresh collagen and from frozen collagen (see FIGS. 2 a and 2 b). Thevariability of results was substantially lower for membranes preparedfrom lyophilised milled collagen, which was stored at a temperature of2-8° C. for 3 years before compounding (old LMC) than for the membranesprepared from fresh collagen and from frozen collagen.

As can be seen in FIG. 6, the thickness change for each collagenmembrane tested demonstrates that the improved water uptake and swellingcharacteristics of membranes prepared from matured lyophilised milledcollagen over membranes prepared from lyophilised milled collagen, whichwas stored at a temperature of 2-8° C. for 3 years before compounding(old LMC), are comparable to the improved water uptake and swellingcharacteristics of membranes prepared from matured lyophilised milledcollagen over membranes prepared from frozen collagen.

The reduced swelling characteristics of membranes prepared from maturedlyophilised milled collagen is advantageous as the membranes may beimplanted into restricted anatomical spaces with a lower risk ofpressurising and potentially damaging vital organs. Thus, for use intreating or preventing surgical adhesions, membranes prepared from themodified collagen may be used in a greater variety of anatomicalgeometries and surgical procedures.

Degradation with Collagenase

Degradation studies were conducted using 4 to 5 membranes per batch ofeach of the fresh collagen, frozen collagen, old lyophilised milledcollagen, and matured lyophilised milled collagen. One membrane (4.5×4.5cm in size) was placed into a beaker and covered with 15 mL of 0.2NPhosphate buffer (pH 7.4 with CaCl₂). Collagenase (Collagenase TypeIA-S, sterile, 50 mg, SIGMA, REF C5894) was reconstituted with 5 mL ofWFI, and 0.5 mL of the resulting solution was added to the mixture. Thesolution in the beaker was agitated using a shaking water bath (JulaboSW 22) at 37° C. (120 rpm) for 60 minutes. The degradation wasdocumented by taking photographs of the samples every 5 minutes. Resultsare shown in Table 1. Membranes prepared from lyophilised milledcollagen degraded the fastest with no residue, while membranes preparedfrom fresh collagen and frozen collagen degraded considerably slower,and left behind small fibre agglomerates.

TABLE 1 Degradation of equine collagen membranes in presence ofCollagenase Frozen Old Lyophilized Fresh Collagen Wet Collagen MilledCollagen Dissolution [min] 50 50 25

In a further study, 3.1×3.1 cm membrane samples were immersed in 15 mLof the buffer described above; to which 100 μL of reconstitutedcollagenase solution was added. 1 mL samples were removed after 5, 10,15, 25, 40, 60, and 90 minutes; samples were filtered through a 0.45 μmsyringe filter, and a 100 μL aliquot was diluted 1:30. UV absorptionspectra between 210 and 230 nm (2 nm increments) were measured against ablank solution using a UV-VIS Photometer Specord 205 (Analytic Jena).The degraded fraction at each time point was calculated from the maximumabsorption relative to the 90 minute time point (defined as 100%). Theresults can be seen in FIG. 7, which illustrated that membranes preparedfrom matured lyophilised milled collagen degraded faster than membranesprepared from lyophilised milled collagen.

A composition for use in treating or preventing surgical adhesions, forexample a membrane for use as an adhesion barrier, needs to stay intactfor a certain time in order to effectively inhibit adhesion. Prolongedpresence of the membrane could lead to increased risk of infections,given that collagen is known to be a medium for bacterial growth. Thesein vitro experiments demonstrate that the membranes prepared frommatured lyophilised milled collagen degrade faster than membranesprepared from old lyophilised milled collagen, and yet faster thanmembranes prepared from fresh collagen and frozen collagen, suggestingthat this effect will also be true for the in vivo behaviour.Accordingly, a composition comprising a modified collagen according to afirst aspect of the present invention, or a modified collagen preparedaccording to a second aspect of the present invention, for use intreating surgical adhesions, can reduce the probability of infections asan adverse effect of the use of the adhesion barrier.

Taken together, the examples provided herein demonstrate that acomposition comprising a modified collagen according to a first aspectof the present invention, or a modified collagen prepared according to asecond aspect of the present invention—for example, membranes preparedfrom matured lyophilised milled collagen—exhibit significantly alteredproperties compared to membranes made from fresh collagen, frozencollagen, or non-matured lyophilised milled collagen. The maturing stepproviding the altered properties of aged collagen without the extendedageing period; and so can be particularly useful in the manufacture ofcompositions for use in preventing or treating surgical adhesions.

Example 4 Dissolution Preparation of Compositions Comprising Gentamicin

Compositions (sponges) containing gentamicin sulfate (Fujian FukangPharmaceutical Co. Ltd, China) were prepared for dissolution testingfrom a 1.6% w/w collagen dispersion using a modified 5 version of themethod described herein above. Each sponge measured 2.5×2.5×0.5 cm andcontained 50 mg of collagen and 50 mg of gentamicin sulfate. In short,gentamicin sulfate (1.6% w/w) and 1N Acetic Acid were added to water forinjection (WFI), and stirred until a clear solution resulted. Collagen(1.6% w/w) was added to the solution, either as frozen collagen (thaweddirectly prior to production); as non-matured Lyophilized MilledCollagen (non-matured LMC; lyophilized directly prior to production); oras a modified collagen according to the present invention (matured LMC).The mixture was homogenized using a commercially available high shearmixer (Ultraturrax, IKA, Germany) for 1 to 5 minutes at a temperaturebetween 38 and 42° C. until a homogeneous viscous dispersion wasobtained. The dispersion was filtered through a 250 μm mesh and stirredfor approximately 30 minutes. Aliquots of the dispersion were filledinto blisters and placed onto the shelves of a suitable freeze dryer andlyophilized. The blisters filled with dispersion were transferred ontothe shelves of a commercially available freeze dryer and frozen to atemperature of about −38° C. with a ramp rate between 0.3° C. and 1.5°C. After an equilibration period of approximately 30 to 60 minutes,vacuum was initiated and the shelf temperature was sequentiallyincreased from about −38° C. to about +30° C. at a rate of about 0.5° C.per minute. The combination of vacuum and sequentially increasing theshelf temperature from about −38° C. to about +30° C. facilitatedsublimation of the ice from the frozen dispersion up until the productreached a temperature of 0° C. To ensure that the temperature of thecollagen increased uniformly, at least one equilibrating step wasconducted, in which the shelf temperature was maintained at a constantdesired temperature for at least 30 mins, or until the collagen reachedthe desired temperature. The sponge-like porous composition was removedfrom the blister cavities and packed in pouches as described in Example2 herein above.

Preparation of Compositions Comprising Bupivacaine

Compositions (sponges) containing bupivacaine HCl were produced fordissolution testing according to a similar method as described above.Sponges were produced from frozen collagen (FWC) and dehydrated frozencollagen, which was allowed to age under ambient conditions for 3 years(old LMC). Each sponge measured 5×5×0.5 cm and contained 75 mg ofcollagen and 100 mg of bupivacaine HCl (see FIG. 3). Sponges were alsoproduced from dehydrated frozen collagen, which was allowed to age underambient conditions for 3 years (old LMC) and dehydrated frozen collagen(non-matured LMC), measuring 10×10×0.5 cm and containing 100 mgbupivacaine-HCl and 300 mg collagen. (see FIG. 8B). In short, 1N AceticAcid was added to WFI and briefly mixed. Collagen (0.6% w/w; eitherfrozen collagen; Lyophilized Milled Collagen; or matured LMC) was addedto the solution. The mixture was homogenized using a commerciallyavailable high shear mixer (Ultraturrax, IKA, Germany) for 1 to 5minutes at a temperature between 38 and 42° C. until a homogeneousviscous dispersion was obtained. The dispersion was filtered through a250 μm mesh.

Bupivacaine HCl (0.8% w/w) was dissolved in a small amount of WFI andadded to the collagen dispersion. The mixture was stirred forapproximately 30 minutes. Aliquots of the dispersion were filled intomoulds and transferred onto the shelves of a commercially availablefreeze dryer and frozen to a temperature of about −38° C. with a ramprate between 0.3° C. and 1.5° C. After an equilibration period ofapproximately 30 to 60 minutes vacuum was initiated and the shelftemperature was sequentially increased from about −38° C. to about +30°C. at a rate of about 0.5° C. per minute. The combination of vacuum andsequentially increasing the shelf temperature from about −38° C. toabout +30° C. facilitated sublimation of the ice from the frozendispersion up until the product reached a temperature of 0° C. To ensurethat the temperature of the collagen increased uniformly, at least oneequilibrating step was conducted, in which the shelf temperature wasmaintained at a constant desired temperature for at least 30 mins, oruntil the collagen reached the desired temperature. The sponge-likeporous compositions were removed from the moulds and packed in pouches,as described in Example 2 herein above.

Gentamicin Dissolution Studies

The dissolution properties of compositions (sponges) containinggentamicin sulfate were analyzed in duplicate using a DissolutionApparatus Type II (Distek Inc., USA), according to the manufacturer'sinstructions. To prevent the sponges from floating, they were placedinto custom-made stainless steel sinkers. The weighted sponges wereimmersed in 500 mL of PBS Buffer (phosphate buffered saline, pH 7.4,bath temperature 37° C.) and stirred at 50 rpm for 24 hours. 4.0 mLsample was removed after 5, 10, 30, 45, 60, 120, 180, 240 and 1440minutes. The samples were subjected to a chemical derivatisationreaction with Phthalaldehyde (4 mL sample +1.6 mL of a solutioncomprising 1% Phthalaldehyde +4.4 mL methanol) at 60° C. for 15 min(dilution 4/10). The resulting solutions were filtered and analyzed in aHPLC system (Shimadzu Corp., Japan), according to the manufacturer'sinstructions. A RP-18 HPLC column and a mobile phase comprising WFI,methanol, acetic acid and Na-1-heptanesulfonate with a flow rate of 0.5mL/min was used. The gentamicin peaks C1, C2 and C2a at 330 nm wereintegrated, and the gentamicin concentration was calculated from thearea under the curve of the samples and from a reference standard thatwas subjected to identical sample preparation.

Bupivacaine Dissolution Studies

The dissolution properties of compositions (sponges) containingbupivacaine HCl were analyzed in duplicate using a Dissolution apparatusType II (Distek Inc., USA), as described above. To prevent the spongesfrom floating, they were placed into custom-made stainless steelsinkers. In short, the weighted sponges were immersed in 500 mL of PBSBuffer (phosphate buffered saline, pH 6.8, bath temperature 37° C.) andstirred with 50 rpm for 24 hours. 4.0 mL sample was removed after 5, 10,30, 45, 60, 120, 180, 240 and 1440 minutes. The samples were diluted 1:1with PBS buffer, filtered and analyzed in a HPLC system (Shimadzu Corp.,Japan). A RP-18 HPLC column and a mobile phase comprising phosphatebuffer pH 4.5 and acetonitrile with a flow rate of 0.5 mL/min was used.The bupivacaine peak at 230 nm was integrated, and the bupivacaineconcentration was calculated from the area under the curve of thesamples and from a reference standard.

The results of the dissolution studies are illustrated in FIGS. 3A, 3B,and 8A and 8B.

The results of these dissolution studies demonstrate that a modifiedcollagen according to the present invention provides a drug deliverycomposition, wherein the rate of release of biologically activesubstances from the collagen-based composition is reduced relative tothose compositions made from isolated collagen without modification,thereby providing a drug delivery composition having a more sustainedaction of drug release (see FIGS. 3A and 3B).

Moreover, as can be seen from FIGS. 8A and 8B, matured LMC provides adrug delivery composition, which demonstrates a significantly reducedrate of release of biologically active substances compared tocompositions prepared from non-matured lyophilised LMC or frozencollagen; thereby providing a drug delivery composition having a moresustained action of drug release.

This extended release can be beneficial for collagen-based productscontaining active pharmaceutical ingredients (API) with good solubilityin water. A retardation of release kinetics for this combination isotherwise difficult to achieve without chemical cross-linking of thedrug delivery composition. Both in topical and implant administration,the extended release of the ingredient from the drug deliverycomposition can lead to longer therapeutic action and improved localefficacy.

Example 5 Storage

Non-matured lyophilized milled collagen (non-matured LMC) was preparedas described in Example 1; and matured by storing in polyethylenecontainers (bags) as described herein for up to 4 weeks. The resultingmaterial was designated matured lyophilized milled collagen (maturedLMC).

The viscosity values were measured at each of the time periods noted (1,2, 3, and 4 weeks storage) as described in Example 3. In short, theviscosity values were measured using a Brookfield viscometer (DigitalRheometer DV-III+ with associated TC-501 Circulating Bath) at a constantshear rate (15 s⁻¹) and over a temperature range from 30 to 65° C. Theviscosity values of matured lyophilised milled collagen having a lowmoisture content of 1-2% and a high moisture content of 13-15% weremeasured.

As can be seen from FIG. 9, generally, the viscosity of the maturedlyophilised milled collagen is unaffected by the moisture content of thematured lyophilised milled collagen. Moreover, increasing the storagetemperature accelerates the viscosity reduction of the maturedlyophilised milled collagen. Certainly, maturing the lyophilised milledcollagen as described herein results in improved viscosity at allinvestigated storage times. At lower storage temperature, the timerequired to reach the target viscosity is extended.

1. A method for preparing a modified collagen, the method comprising the steps of: (a) providing isolated collagen; (b) freezing the isolated collagen; and (c) dehydrating the frozen collagen.
 2. The method of claim 1, further comprising the step of (d) maturing the dehydrated collagen.
 3. The method of claim 1, wherein the providing step comprises the step of removing the fluid prior to the providing step to provide a dispersion having a concentration of about 3-30% (w/w) collagen particles.
 4. The method of claim 1, wherein the freezing step comprises freezing to a temperature of about −33° C. to about −42° C.
 5. The method of claim 1, wherein the dehydrating step comprises removing the aqueous phase by reducing the pressure to about 0.05 to about 0.5 mbar.
 6. The method of claim 1, wherein the dehydrating step comprises increasing the temperature of the collagen to about +30° C.
 7. The method of claim 1, wherein the dehydrating step comprises at least one equilibrating step, wherein the or each equilibrating step comprises maintaining the temperature at a constant temperature for at least 10 minutes.
 8. (canceled)
 9. The method of claim 2, wherein the maturing step comprises storing the dehydrated collagen at a temperature of at least 2° C.
 10. The method of claim 2, wherein the maturing step is conducted for a period of at least one week.
 11. The method claim 2, wherein the maturing step comprises storing the dehydrated collagen at a temperature of at least 2° C. for a period of at least six months.
 12. The method claim 2, wherein the maturing step comprises storing the dehydrated collagen at a temperature of at least 30° C. for a period of at least two months.
 13. The method claim 2, wherein the maturing step comprises storing the dehydrated collagen at a temperature of at least 40° C. for a period of at least six weeks.
 14. The method claim 2, wherein the maturing step comprises storing the dehydrated collagen at a temperature of at least 65° C. for a period of at least one week.
 15. The method of claim 1, wherein the maturing step is conducted at a relative humidity of less than 80%.
 16. A modified collagen obtained from the method of claim
 11. 17. A method of treating or preventing surgical adhesions, the method comprising administering a composition comprising the modified collagen of claim 16 at a biological membrane.
 18. (canceled)
 19. A method for the manufacture of a composition, the method comprising the steps of: (a) providing the modified collagen of claim 16; (b) preparing an aqueous dispersion of the modified collagen; (c) degrading the aqueous dispersion; and (d) dehydrating the aqueous dispersion.
 20. The method of claim 19, wherein the preparing step comprises adding water heated to about 35 to about 42° C. to the modified collagen, prior to adding to the modified collagen. 21-26. (canceled) 